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  • C01B21/00—Nitrogen; Compounds thereof
  • C01B21/06—Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron
  • C01B21/068—Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron with silicon
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  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01D69/12—Composite membranes; Ultra-thin membranes
  • B01D69/1216—Three or more layers
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  • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
  • B01D61/002—Forward osmosis or direct osmosis
  • B01D61/0022—Apparatus therefor
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  • B01D61/42—Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
  • B01D61/44—Ion-selective electrodialysis
  • B01D61/46—Apparatus therefor
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  • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
  • B01D63/08—Flat membrane modules
  • B01D63/088—Microfluidic devices comprising semi-permeable flat membranes
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  • B01D67/0002—Organic membrane manufacture
  • B01D67/0023—Organic membrane manufacture by inducing porosity into non porous precursor membranes
  • B01D67/0032—Organic membrane manufacture by inducing porosity into non porous precursor membranes by elimination of segments of the precursor, e.g. nucleation-track membranes, lithography or laser methods
  • B01D67/0034—Organic membrane manufacture by inducing porosity into non porous precursor membranes by elimination of segments of the precursor, e.g. nucleation-track membranes, lithography or laser methods by micromachining techniques, e.g. using masking and etching steps, photolithography
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  • B01D67/0039—Inorganic membrane manufacture
  • B01D67/0053—Inorganic membrane manufacture by inducing porosity into non porous precursor membranes
  • B01D67/006—Inorganic membrane manufacture by inducing porosity into non porous precursor membranes by elimination of segments of the precursor, e.g. nucleation-track membranes, lithography or laser methods
  • B01D67/0062—Inorganic membrane manufacture by inducing porosity into non porous precursor membranes by elimination of segments of the precursor, e.g. nucleation-track membranes, lithography or laser methods by micromachining techniques, e.g. using masking and etching steps, photolithography
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  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
  • B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01D69/1213—Laminated layers
• • B—PERFORMING OPERATIONS; TRANSPORTING
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  • B01D69/14—Dynamic membranes
  • B01D69/141—Heterogeneous membranes, e.g. containing dispersed material; Mixed matrix membranes
  • B01D69/148—Organic/inorganic mixed matrix membranes
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  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
  • B01D71/02—Inorganic material
  • B01D71/021—Carbon
  • B01D71/0211—Graphene or derivates thereof
• • B—PERFORMING OPERATIONS; TRANSPORTING
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  • B01D71/02—Inorganic material
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• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01D71/02—Inorganic material
  • B01D71/0215—Silicon carbide; Silicon nitride; Silicon oxycarbide
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  • C01B19/00—Selenium; Tellurium; Compounds thereof
  • C01B19/007—Tellurides or selenides of metals
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  • C01B21/00—Nitrogen; Compounds thereof
  • C01B21/06—Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron
  • C01B21/068—Binary compounds of nitrogen with metals, with silicon, or with boron, or with carbon, i.e. nitrides; Compounds of nitrogen with more than one metal, silicon or boron with silicon
  • C01B21/0682—Preparation by direct nitridation of silicon
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  • C01B32/00—Carbon; Compounds thereof
  • C01B32/15—Nano-sized carbon materials
  • C01B32/182—Graphene
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  • C01B32/00—Carbon; Compounds thereof
  • C01B32/20—Graphite
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  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B32/00—Carbon; Compounds thereof
  • C01B32/20—Graphite
  • C01B32/21—After-treatment
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
  • C02F1/445—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by forward osmosis
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
  • C02F1/447—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by membrane distillation
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
  • C02F1/4693—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F1/00—Treatment of water, waste water, or sewage
  • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
  • C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
  • C02F1/4698—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electro-osmosis
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2313/00—Details relating to membrane modules or apparatus
  • B01D2313/14—Specific spacers
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01D2325/02—Details relating to pores or porosity of the membranes
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• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01D2325/02833—Pore size more than 10 and up to 100 nm
• • B—PERFORMING OPERATIONS; TRANSPORTING
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  • B01D2325/02834—Pore size more than 0.1 and up to 1 µm
• • B—PERFORMING OPERATIONS; TRANSPORTING
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• • B—PERFORMING OPERATIONS; TRANSPORTING
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  • B01D2325/26—Electrical properties
• • B—PERFORMING OPERATIONS; TRANSPORTING
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• • B—PERFORMING OPERATIONS; TRANSPORTING
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• • B—PERFORMING OPERATIONS; TRANSPORTING
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  • B01D—SEPARATION
  • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
  • B01D61/002—Forward osmosis or direct osmosis
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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  • B01D61/42—Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
  • B01D61/44—Ion-selective electrodialysis
  • B01D61/46—Apparatus therefor
  • B01D61/48—Apparatus therefor having one or more compartments filled with ion-exchange material, e.g. electrodeionisation
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/40—Electric properties
• • C—CHEMISTRY; METALLURGY
  • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
  • C02F2303/00—Specific treatment goals
  • C02F2303/10—Energy recovery
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
  • Y02W10/00—Technologies for wastewater treatment
  • Y02W10/30—Wastewater or sewage treatment systems using renewable energies

Definitions

• the present invention relates to a multi-layered membrane comprising a top layer, a bottom layer and a spacer layer.
• the present invention also relates to a method to synthesize the top layer of the multi-layered membrane as disclosed herein, methods for separating a plurality of ions or molecules in a fluid stream, a device comprising a multi-layered membrane, and use of the method or the device as disclosed herein in osmotic power generation.
• Two-dimensional (2D) materials can be used to create membranes comprising nanocavities, for example, nanochannels, nanopores, or nanotubes, with critical dimension as low as 0.3 nm. Ions and water molecules inside these nanocavities behave differently than in the bulk phase because of their physical confinement and strong interaction with the surface of these nanocavities, resulting in different ionic mobilities compared to their bulk phase and different mobilities between cations and anions.
• the present disclosure relates to a multi-layered membrane comprising a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; wherein the bottom layer comprises a hole with an area in the range of 1 pm 2 to 1 mm 2 ; and wherein the hole is capable of being in fluid communication with the at least one channel of the spacer layer.
• the multi-layered membrane as disclosed herein may be intrinsically uncharged and therefore, may be energy-free, offering the multi-layered membrane an additional degree of freedom to be engineered for its ionic selectivity.
• the ionic selectivity of the multi-layered membrane may be tuned based on the dimension of the channel and the type of 2D material used.
• the multi-layered membrane as disclosed herein may possess atomically smooth surfaces comprising channels in the critical dimension ranging from about 0.3 nm to about 250 nm, which may enable the multi-layered membrane to be ionic and/or charge selective by selectively enhancing the mobility of cations and/or anions in the channels with respect to their mobility in the bulk.
• This may be attributed to the interaction between the cations and anions with the surfaces of the channels which is dependent on the intrinsic property of the channels’ surfaces as well as the degree of physical confinement of the cations and anions in the channels.
• the enhanced mobility of the cations and/or anions may be independent of surface charge or roughness of the channels.
• the multi-layered membrane with its enhanced mobility of the cations or anions than the respective counter ion may result in the counter-ion rejection which does not affect the water permeation properties of the multi layered membrane.
• the multi-layered membrane as disclosed herein with its enhanced ionic mobility may in turn enhance ionic conductivity of the solution regardless of the pH of the ionic or electrolyte solution, since ionic conductivity is significantly related to the ionic diffusivity at the surface. This is because the interaction between the walls of channels and ions in an electrolyte solution may occur via delocalized p-electrons on the walls of the channels (for example, walls of graphene), giving rise to preferential absorption of cations.
• the preferential absorption of the cations may be combined with the preferred alignment of water molecules in the near-surface region, resulting in the enhanced diffusivity of cations and reduced flow of anions in a cation selective multi-layered membrane, or enhanced diffusivity of anions and reduced flow of cations in an anion selective multi-layered membrane.
• the width of the hole in the bottom layer may influence the thickness of the top layer, as the larger the width of the hole in the bottom layer, the thicker the thickness of the top layer may be required to prevent the bending of the selective layers within the top layer, which may in turn impact the overall multi-layered membrane performance.
• the width of the hole in the bottom layer is reduced, it may allow a thinner top layer to be used without any unwanted bending effects.
• the multi-layered membrane as disclosed herein may be deposited on a support or embedded in a matrix, to serve as an active multi-layered membrane when it is incorporated into another membrane or system.
• the multi-layered membrane as disclosed herein may be about 30 times cheaper and may generate about 1000 times more power for the same surface area compared to conventional membranes, thus making it cost effective and energy efficient for commercial applications.
• the present disclosure relates to a method to synthesize a top layer of a multi-layered membrane as disclosed herein, comprising the steps of: (a) providing a spacer layer/bottom layer assembly; (b) dry transferring a selective layer comprising a 2D material on top of the spacer layer of the spacer layer/bottom layer assembly; (c) depositing a metal layer or metal oxide layer on top of the selective layer of step (a) to form a mask; and (d) subjecting the metal layer or metal oxide layer to an etching process.
• the present disclosure relates to a method for separating a plurality of ions or molecules in a fluid stream comprising the steps of: a) providing a multi-layered membrane; b) contacting a first surface of the multi-layered membrane with the fluid stream under a driving force to selectively allow desired ions or molecules to pass through to a second surface; wherein first surface of the multi-layered membrane is optionally charged; and wherein the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; and wherein bottom layer comprises a hole that is capable of being in fluid communication with the at least one channel of the spacer layer.
• the present disclosure relates to a method for separating a plurality of ions or molecules in a fluid stream comprising the steps of: a) providing a multi-layered membrane; b) contacting a first surface of the multi-layered membrane with the fluid stream under a driving force to selectively allow desired ions or molecules to pass through to a second surface; wherein first surface of the multi-layered membrane is optionally charged; and wherein the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; wherein the bottom layer comprises a hole with an area in the range of 1 pm 2 to 1 mm 2 ; and wherein the hole is capable of being in fluid communication with the at least one channel of the spacer layer.
• the method as disclosed herein comprises the use of a multi-layered membrane which has ionic selectivity, an osmotic voltage and / or an osmotic current may be generated and thus, the method may be suitable for blue energy generation and storage where there is salinity gradient, for example in water desalination plants, nanofiltration, ion-exchange, brine-disposal and water filtration operations, and may find many commercial applications in water purification, pharmaceutical, chemical and fuel separation industries.
• the present disclosure relates to a device comprising a multi-layered membrane comprising a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; wherein the bottom layer comprises a hole with an area in the range of 1 pm 2 to 1 mm 2 ; and wherein said hole is capable of being in fluid communication with the at least one channel of the spacer layer.
• the device as disclosed herein may be used for energy recovery.
• the device as disclosed herein may form part of an electrodialysis system or reverse electrodialysis, when two sets of multi-layered membranes as defined herein have opposite charge selectivity.
• the present disclosure relates to use of the method or the device as disclosed herein in osmotic power generation.
• a device comprising a multi-layered membrane for osmotic power generation wherein the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; and wherein the bottom layer comprises a hole that is capable of being in fluid communication with the at least one channel of the spacer layer.
• 2D material refers to a single-layered material which is crystalline and consists of a single layer of atoms.
• nanochannels refers to channels which are dimensioned in the nanometre- size range from 0.1 nanometre to hundreds of nanometres.
• ionic mobility refers to the speed achieved by an ion when moving through a substance in response to an electrochemical gradient.
• ionic conductance refers to the physical property of a substance denoting the ease of which an ion transmits from one site to another.
• difference number refers to ion transport number, which is the fraction of the total electrical current carried in an electrolyte by a given ionic species, where difference in transference number arises from difference in ionic mobility.
• graphene refers to an allotrope of carbon consisting of a single layer of atoms arranged in a two-dimensional hexagonal array, wherein each atom in the graphene sheet is connected to its three nearest neighbours by a s-bond, and contributes one electron to a conduction band that extends over the whole layer.
• graphite refers to a type of crystal carbon composing of more than ten graphene layers stacked loosely.
• blue energy refers to osmotic power which occurs in a concentration cell with salinity gradient across two sides, and a semi -permeable membrane in between the two sides capturing the electrochemical potential generated into energy due to the movement of the water molecules between the two sides.
• the term "about”, in the context of concentrations of components of the formulations, typically means +/- 5% of the stated value, more typically +/- 4% of the stated value, more typically +/- 3% of the stated value, more typically, +/- 2% of the stated value, even more typically +/- 1% of the stated value, and even more typically +/- 0.5% of the stated value.
• range format is merely for convenience and brevity and should not be construed as an inflexible limitation on the scope of the disclosed ranges. Accordingly, the description of a range should be considered to have specifically disclosed all the possible sub ranges as well as individual numerical values within that range. For example, description of a range such as from 1 to 6 should be considered to have specifically disclosed sub -ranges such as from 1 to 3, from 1 to 4, from 1 to 5, from 2 to 4, from 2 to 6, from 3 to 6 etc., as well as individual numbers within that range, for example, 1, 2, 3, 4, 5, and 6. This applies regardless of the breadth of the range.
• the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; wherein the bottom layer comprises a hole with an area in the range of about 1 pm 2 tol mm 2 ; and wherein the hole is capable of being in fluid communication with the at least one channel of the spacer layer.
• the area of the hole may alternatively be in the range of about 10 pm 2 to about 1 mm 2 , about 100 pm 2 to about 1 mm 2 , about 1000 pm 2 to about 1 mm 2 , about 0.01 mm 2 to about 1 mm 2 , about 0.1 mm 2 to about 1 mm 2 , about 1 pm 2 to about 10 pm 2 , about 1 pm 2 to about 100 pm 2 , about 1 pm 2 to about 1000pm 2 , about 1 pm 2 to about 0.01 mm 2 , about 1 pm 2 to about 0.1 mm 2 , about 10 pm 2 to about 100 pm 2 , about 10 pm 2 to about 1000pm 2 , about 10 pm 2 to about 0.01 mm 2 , about 10 pm 2 to about 0.1 mm 2 , about 100 pm 2 to about 1000pm 2 , about 100 pm 2 to about 0.01 mm 2 , about 100 pm 2 to about 0.1 mm 2 , about 1000 pm 2 to about 0.01 mm 2 , about 1000 pm 2 to about 0.1 mm 2 , about 100 pm 2 to about 1000
• the width of the hole may be in the range of about 20 nm to about 2 pm, about 100 nm to about 2 pm, about 500 nm to about 2 pm, about 1 pm to about 2 pm, about 1.5 pm to about 2 pm, about 20 nm to about 100 nm, about 20 nm to about 500 nm, about 20 nm to about 1 pm, about 20 nm to about 1.5 pm, about 100 nm to about 500 nm, about 100 nm to about 1 pm, about 100 nm to about 1.5 pm, about 500 nm to about 1 pm, about 500 nm to about 1.5 pm, or about 500 nm to about 1.5 pm; and the length of the hole may be in the range of about 20 nm to about 1 mm, about 100 nm to about 1 mm, about 1000 nm to about 1 mm, about 0.001 mm to about 1 mm, about 0.01 mm to about 1 mm, about 0.1 mm to about 1 mm, about 20 nm to about 100 nm
• top layer and bottom layer can be regarded as relative terms that depend on the orientation by which the multi-layered membrane is viewed at, as long as the layer is one that contains a hole, that layer is to be regarded as the “bottom layer” regardless of whether it is seen as the first layer when viewed according to a certain orientation (for example, when viewing the membrane from the bottom, the first layer would still be regarded as the “bottom layer” and not the “top layer” as it is the layer with the hole therein).
• the 2D material may be a nanoparticle.
• the 2D material may be selected from the group consisting of graphene, graphite, hexagonal boron nitride, transition metal dichalcogenide, phosphorene, xene, transitional metal-xene and combinations thereof.
• the 2D material may preferably be one or more layers of graphene.
• the 2D material may be graphite which may be composed of more than ten graphene layers.
• the transition metal dichalcogenide has a chemical formula MX2, wherein M may be a transition metal selected from the group consisting of titanium, vanadium, chromium, manganese, zirconium, niobium, molybdenum, technetium, hafnium, tantalum, tungsten and rhenium; and wherein X may be a chalcogen selected from the group consisting of sulfur, selenium and tellurium.
• the xene may be selected from the group consisting of borophene, silicene, germanene, stanene, phosphorene, arsenene, antimonene, bismuthene, and tellurene.
• the transition metal-xene may be selected from the group consisting of mono or double transition metal-xene.
• the channels may be nanochannels.
• the channels may be straight, percolative or combinations thereof.
• the shape of the channels may depend on the type of 2D material used. When the 2D material is graphene, the channels may be straight.
• the shape of the hole in the bottom layer may not be particularly limited and may be a square, a rectangle or a circle.
• the width of the hole in the bottom layer may influence the thickness of the top layer, as the larger the width of the hole in the bottom layer, the thicker the thickness of the top layer may be required to prevent the bending of the selective layers within the top layer, which may in turn impact the overall multi-layered membrane performance.
• the width of the hole in the bottom layer is reduced, it may allow a thinner top layer to be used without any unwanted bending effects.
• the bottom layer or spacer layer may independently comprises one or more layers of a substrate, which may be present during formation of the layers but which may be removed when combining the layers together during multi-layered membrane formation.
• the substrate may be independently selected from the group consisting of silicon, silicon nitride (SiNx), silicon oxide (S1O2), alumina (AI2O3), anodic aluminium oxide, aluminium oxide, titanium dioxide, hafnium dioxide, nylon, polymer, polyether sulfone, polyvinyl alcohol (PVA), polycarbonate (PC), and polyvinylidene fluoride.
• the use of silicon oxide as a reflecting substrate may enhance optical contrast and hence allow the selective layers of the bottom layer or spacer layer to be visible for ease of identification during multi-layered membrane synthesis, such as after the step of mechanical exfoliation.
• the silicon oxide substrate may have a thickness in the range of about 80 nm to about 500nm, and preferably at about 300 nm.
• the bottom layer comprising one or more layers of substrate may be supported on the surface of the one or more layers of substrate.
• the one or more layers of substrate may improve the overall mechanical strength of the structure of the multi-layered membrane.
• the one or more layers of substrate function(s) as a mechanical support for the bottom layer. It is to be noted that reference to the hole in the bottom layer (or reference to the dimension of the hole in the bottom layer, such as area, width or length of the hole) is regarded as the hole present in the bottom layer that is made up of the 2D material, and not to the hole in the substrate of the bottom layer.
• the top layer, bottom layer or spacer layer may be optionally subjected to surface chemical functionalization, forming a top layer, bottom layer or spacer layer that is surface-functionalized.
• the surface chemical functionalization may alter the properties of the selective layer.
• the surface chemical functionalization may be applied on the surfaces, entries or exits of the selective layers of the top layer, bottom layer or spacer layer.
• the surface chemical functionalization may enhance the hydrophilicity or hydrophobicity of the top layer, bottom layer or spacer layer. Therefore, the surface-functionalised top layer, surface- functionalised bottom layer or spacer surface -functionalised layer may have a different hydrophilicity or hydrophobicity as compared to a non surface-functionalized corresponding layer.
• Surface chemical functionalization may be undertaken using different chemical groups to enhance the performance of the membrane such as to increase the selectivity towards targeted ions or molecules, or to reduce fouling of the multi-layered membrane.
• the surface chemical functionalization may be selected from the group consisting of hydrogenation, fluorination, oxidation, silanization, hydroxylation and carboxylation.
• the treated graphene layer may be more hydrophilic than the untreated graphene layer.
• the treated graphene layer may be more hydrophobic than the untreated graphene layer.
• the bottom layer, top layer or spacer layer may be patterned or etched.
• the bottom layer comprising one or more layers of substrate may be patterned or etched.
• the bottom layer, spacer layer and top layer may each compose of a graphitic layer, thus forming a first (bottom) graphitic layer, a second (spacer) graphitic layer, and a third (top) graphitic layer respectively.
• the first (bottom) graphitic layer may be supported on one or more layers of substrate.
• the substrates used for the first (bottom) graphitic layer may preferably be a layer of silicon nitride (SiNx) substrate and a layer of silicon (Si) substrate.
• the layer of silicon substrate may be beneath the layer of silicon nitride substrate.
• the area of the bottom graphitic layer may be in the range of about 1 pm 2 to about 10 mm 2 , about 10 pm 2 to about 10 mm 2 , about 100 pm 2 to about 10 mm 2 , about 1000 pm 2 to about 10 mm 2 , about 0.01 mm 2 to about 10 mm 2 , about 0.1 mm 2 to about 10 mm 2 , about 1 mm 2 to about 10 mm 2 , about 1 pm 2 to about 10 pm 2 , about 1 pm 2 to about 100 pm 2 , about 1 pm 2 to about 1000 pm 2 , about 1 pm 2 to about 0.01 mm 2 , about 1 pm 2 to about 0.1 mm 2 , about 1 pm 2 to about 1 mm 2 , about 10 pm 2 to about 100 pm 2 , about 10 pm 2 to about 1000 pm 2 , about 10 pm 2 to about 0.01 mm 2 , about 10 pm 2 to about 0.1 mm 2 , about 10 pm 2 to about 100 pm 2 , about 10 pm 2 to about 1000 pm 2 , about 10 pm 2 to about 0.01
• the width of the bottom graphitic layer may be about 100 nm to about 1 mm, about 1000 nm to about 1 mm, about 0.001 mm to about 1 mm, about 0.01 mm to about 1 mm, about 0.1 mm to about 1 mm, about 100 nm to about 1000 nm, about 100 nm to about 0.001 mm, about 100 nm to about 0.01 mm, about 100 nm to about 0.1 mm, about 1000 nm to about 0.001 mm, about 1000 nm to about 0.01 mm, about 1000 nm to about 0.1 mm, about 0.001 mm to about 0.01 mm, about 0.001 mm to about 0.1 mm, or about 0.01 mm to about 0.1 mm larger than the width of the hole in the SiNx substrate layer.
• the length of the bottom graphitic layer may be about 100 nm to about 1 mm, about 1000 nm to about 1 mm, about 0.001 mm to about 1 mm, about 0.01 mm to about 1 mm, about 0.1 mm to about 1 mm, about 100 nm to about 1000 nm, about 100 nm to about 0.001 mm, about 100 nm to about 0.01 mm, about 100 nm to about 0.1 mm, about 1000 nm to about 0.001 mm, about 1000 nm to about 0.01 mm, about 1000 nm to about 0.1 mm, about 0.001 mm to about 0.01 mm, about 0.001 mm to about 0.1 mm, or about 0.01 mm to about 0.1 mm larger than the length of the hole in the SiNx substrate layer.
• the thickness of said silicon nitride substrate may be in the range of about 10 nm to about 500 nm, about 50 nm to about 500 nm, about 100 nm to about 500 nm, about 200 nm to about 500 nm, about 300 nm to about 500 nm, about 400 nm to about 500 nm, about 10 nm to about 50 nm, about 10 nm to about 100 nm, about 10 nm to about 200 nm, about 10 nm to about 300 nm, about 10 nm to about 400 nm, about 50 nm to about 100 nm, about 50 nm to about 200 nm, about 50 nm to about 300 nm, about 50 nm to about 400 nm, about 100 nm to about 200 nm, about 100 nm to about 300 nm, about 100 nm to about 400 nm, about 100 nm to about 200 nm, about 100 nm to about 300
• the selective layer in the spacer layer may have the following dimensions: a length in the range of about 100 nm to about 1 mm, about 1 pm to about 1 mm, about 5 pm to about 1 mm, about 10 pm to about 1 mm, about 50 pm to about 1 mm, about 100 pm to about 1 mm, about 0.5 mm to about 1 mm, about 100 nm to about 1 pm, about 100 nm to about 5 pm, about 100 nm to about 10 pm, about 100 nm to about 50 pm, about 100 nm to about 100 pm, about 100 nm to about 0.5 mm, about 1 pm to about 5 pm, about 1 pm to about 10 pm, about 1 pm to about 50 pm, about 1 pm to about 100 pm, about 1 pm to about 0.5 mm, about 5 pm to about 10 pm, about 5 pm to about 50 pm, about 5 pm to about 100 pm, about 5 pm to about 0.5 mm, about 10 pm to about 50 pm, about 10 pm to about 100 pm, about 10 pm to about 100 pm, about 10 pm to
• the spacer layer is composed of more than one selective layer to form a stack of selective layers
• this stack can be divided by patterning or etching to form multiple stacks of selective layers.
• the multiple stacks of selective layers may be arranged in an array on the bottom layer to form the spacer layer.
• the distance between one stack of selective layers from another stack of selective layers in the spacer layer may form the width of a channel in the spacer layer.
• the multiple stacks of selective layers in the spacer layer may be oriented perpendicular to the longer side of the rectangle hole in the bottom layer.
• the width and height of the channels may affect the structural stability of the stacks of selective layers in the spacer layer due to the degree of Van der Waals forces between the stacks of selective layers.
• the height of each stack of selective layers in the spacer layer may determine the height of the channels in the multi-layered membrane.
• the spacer layer may contain at least one channel of height equivalent to the height of a stack of selective layers in the spacer layer.
• the spacer layer may contain at least one channel of height in the range of about 0.3 nm to about 300 nm, about 1 nm to about 300 nm, about 10 nm to about 300 nm, about 50 nm to about 300 nm, about 100 nm to about 300 nm, about 200 nm to about 300 nm, about 0.3 nm to about 1 nm, about 0.3 nm to 10 nm, about 0.3 nm to 50 nm, about 0.3 nm to about 100 nm, about 0.3 nm to about 200 nm, about 1 nm to about 10 nm, about 1 nm to about 50 nm, about 1 nm to about 100 nm, about 1 nm to about 200 nm, about 10 nm to about 50 nm, about 10 nm to about 100 nm, about 10 nm to about 200 nm, about 50 nm to about 100 nm, about 50 nm to
• the height of the at least one channel in the spacer layer may be adjusted such that it is comparable, bigger or smaller than the hydrated ionic diameter of ions so that the multi-layered membrane may be selective towards these ions.
• the height of the at least one channel may be about 0.5 to about 1.3 times, such as 0.5 times, 0.6 times, 0.7 times, 0.8 times, 0.9 times, 1.0 times, 1.1 times, 1.2 times or 1.3 times the hydrated ion diameter.
• the top layer may comprise a masked graphitic layer comprising a metal layer or metal oxide layer.
• the metal of the metal layer or the metal oxide layer may be selected from the group consisting of gold, platinum, copper, aluminium, silver, titanium, hafnium and silicon dioxide.
• the first (bottom) graphite crystal may be transferred onto the surface of the SiNx substrate of a SiNx substrate-Si substrate assembly, and the resulting bottom layer may be etched via dry etching such as reactive ion etching using the hole in SiNx substrate as an etch mask.
• the second (spacer) graphitic layer may be formed via exfoliation and may be patterned thereafter by electron beam lithography and/or wet etching or dry etching, wherein the preferred process may be electron beam lithography and dry etching.
• the layers Prior to assembling the bottom layer and the second graphitic layer to form the spacer layer/bottom layer assembly, the layers may be annealed at a suitable temperature ranging from 200 °C to 500 °C, such as about 200 °C, about 250 °C, about 300 °C, about 350 °C, about 400 °C, about 450 °C, or about 500 °C, or values in between. Processing contaminants such as hydrocarbons and polymer residues may be removed at this annealing step.
• the preferred temperature for annealing may be 400 °C.
• the stacks of selective layers may be released from the substrate of the spacer layer by a wet etching process, and may be transferred with a polymeric film on top of the bottom layer by a custom-made micromanipulator.
• the polymeric film may be removed from the stacks of selective layers by dipping the sample in solvent such as acetone and isopropyl alcohol, followed by another step of annealing at about 400 °C.
• the thickness of the substrate may be in the range of about 80 nm to about 500 nm, about 100 nm to about 500 nm, about 200 nm to about 500 nm, about 300 nm to about 500 nm, about 400 nm to about 500 nm, about 80 nm to about 100 nm, about 80 nm to about 200 nm, about 80 nm to about 300 nm, about 80 nm to about 400 nm, about 100 nm to about 200 nm, about 100 nm to about 300 nm, about 100 nm to about 400 nm, about 200 nm to about 300 nm, about 200 nm to about 400 nm, or about 300 nm to about 400 nm.
• the preferred thickness of the S1O2 substrate may be 300 nm.
• the method to synthesize a top layer of the multi-layered membrane as disclosed herein comprises the steps of: (a) providing a spacer layer/bottom layer assembly; (b) dry transferring a selective layer comprising a 2D material on top of the spacer layer of the spacer layer/bottom layer assembly; (c) depositing a metal layer or metal oxide layer on top of said selective layer of step (b) to form a mask; and (d) subjecting the metal layer or metal oxide layer to an etching process.
• the metal of the metal layer or the metal oxide layer may be selected from the group consisting of gold, platinum, copper, aluminium, silver, titanium, hafnium and silicon dioxide.
• the metal layer or the metal oxide layer may enhance the mechanical stability of the entire multi-layered membrane by holding the spacer layer/bottom layer assembly securely on the one or more layers of substrate of the bottom.
• the metal layer or the metal oxide layer may also be an etch mask that protects the multi-layered membrane from the final etching process.
• the process of etching using the metal layer or metal oxide layer as the etching mask may define the final length of the channels in the multi-layered membrane.
• the channels in the multi-layered membrane may be formed by dry etching.
• the part of the spacer layer in the spacer layer/bottom layer assembly covered by the etching mask may be protected from etching, while the remaining part of the spacer layer in the spacer layer/bottom layer assembly not covered by the etching mask may be attacked by the etching gas and may be removed at the end of the etching process to form spacer layer that may be trimmed at the ends.
• the process of etching using the metal layer or metal oxide layer as the etching mask may result in the ends of the spacer layer being trimmed to be flushed with the top layer, which may result in a better fit of the multi-layer membrane to a device.
• the bottom layer (containing the 2D material) can also be etched so as to also be flushed with both the top layer and spacer layer, with the width of the bottom layer (containing the 2D material) being the same as that of the spacer layer and top layer.
• the length of the bottom layer (containing the 2D material) is then regarded as that of the entire bottom layer (containing the 2D material) including the hole portion.
• the method for separating a plurality of ions or molecules in a fluid stream comprising the steps of: a) providing a multi-layered membrane; b) contacting a first surface of the multi-layered membrane with the fluid stream under a driving force to selectively allow desired ions or molecules to pass through to a second surface; wherein first surface of the multi-layered membrane is optionally charged; and wherein the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; and wherein the bottom layer comprises a hole that is capable of being in fluid communication with the at least one channel of the spacer layer.
• the method for separating a plurality of ions or molecules in a fluid stream comprising the steps of: a) providing a multi-layered membrane; b) contacting a first surface of the multi-layered membrane with the fluid stream under a driving force to selectively allow desired ions or molecules to pass through to a second surface; wherein first surface of the multi-layered membrane is optionally charged; and wherein the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; wherein the bottom layer comprises a hole with an area in the range of 1 pm 2 to 1 mm 2 ; and wherein the hole is capable of being in fluid communication with the at least one channel of the spacer layer
• the area of the hole may alternatively be in the range of about 10 pm 2 to about 1 mm 2 , about 100 pm 2 to about 1 mm 2 , about 1000 pm 2 to about 1 mm 2 , about 0.01 mm 2 to about 1 mm 2 , about 0.1 mm 2 to about 1 mm 2 , about 1 pm 2 to about 10 pm 2 , about 1 pm 2 to about 100 pm 2 , about 1 pm 2 to about 1000pm 2 , about 1 pm 2 to about 0.01 mm 2 , about 1 pm 2 to about 0.1 mm 2 , about 10 pm 2 to about 100 pm 2 , about 10 pm 2 to about 1000pm 2 , about 10 pm 2 to about 0.01 mm 2 , about 10 pm 2 to about 0.1 mm 2 , about 100 pm 2 to about 1000pm 2 , about 100 pm 2 to about 0.01 mm 2 , about 100 pm 2 to about 0.1 mm 2 , about 1000 pm 2 to about 0.01 mm 2 , about 1000 pm 2 to about 0.1 mm 2 , about 100 pm 2 to about 1000
• the width of the hole may be in the range of about 20 nm to about 2 pm, about 100 nm to about 2 pm, about 500 nm to about 2 pm, about 1 pm to about 2 pm, about 1.5 pm to about 2 pm, about 20 nm to about 100 nm, about 20 nm to about 500 nm, about 20 nm to about 1 pm, about 20 nm to about 1.5 pm, about 100 nm to about 500 nm, about 100 nm to about 1 pm, about 100 nm to about 1.5 pm, about 500 nm to about 1 pm, about 500 nm to about 1.5 pm, or about 500 nm to about 1.5 pm; and the length of the hole may be in the range of about 20 nm to about 1 mm, about 100 nm to about 1 mm, about 1000 nm to about 1 mm, about 0.001 mm to about 1 mm, about 0.01 mm to about 1 mm, about 0.1 mm to about 1 mm, about 20 nm to about 100 nm
• the selective layer in the spacer layer may have the following dimensions: a length in the range of about 100 nm to about 1 mm, about 1 pm to about 1 mm, about 5 pm to about 1 mm, about 10 pm to about 1 mm, about 50 pm to about 1 mm, about 100 pm to about 1 mm, about 0.5 mm to about 1 mm, about 100 nm to about 1 pm, about 100 nm to about 5 pm, about 100 nm to about 10 pm, about 100 nm to about 50 pm, about 100 nm to about 100 pm, about 100 nm to about 0.5 mm, about 1 pm to about 5 pm, about 1 pm to about 10 pm, about 1 pm to about 50 pm, about 1 pm to about 100 pm, about 1 pm to about 0.5 mm, about 5 pm to about 10 pm, about 5 pm to about 50 pm, about 5 pm to about 100 pm, about 5 pm to about 0.5 mm, about 10 pm to about 50 pm, about 10 pm to about 100 pm, about 10 pm to about 100 pm, about 10 pm to
• the spacer layer may contain at least one channel of height in the range of about 0.3 nm to about 300 nm, about 1 nm to about 300 nm, about 10 nm to about 300 nm, about 50 nm to about 300 nm, about 100 nm to about 300 nm, about 200 nm to about 300 nm, about 0.3 nm to about 1 nm, about 0.3 nm to 10 nm, about 0.3 nm to 50 nm, about 0.3 nm to about 100 nm, about 0.3 nm to about 200 nm, about 1 nm to about 10 nm, about 1 nm to about 50 nm, about 1 nm to about 100 nm, about 1 nm to about 200 nm, about 10 nm to about 50 nm, about 10 nm to about 100 nm, about 10 nm to about 200 nm, about 50 nm to about 100 nm, about 50 nm to
• the height of the at least one channel in the spacer layer may be adjusted such that it is comparable, bigger or smaller than the hydrated ionic diameter of ions so that the multi-layered membrane may be selective towards these ions.
• the height of the at least one channel may be about 0.5 to about 1.3 times, such as 0.5 times, 0.6 times, 0.7 times, 0.8 times, 0.9 times, 1.0 times, 1.1 times, 1.2 times or 1.3 times the hydrated ion diameter.
• step (a) provides a plurality of multi-layered membranes for separating a plurality of ions or molecules in a fluid stream.
• the method may generate osmotic voltage and/or osmotic current due to the differential ionic mobilities induced between the cations and anions as compared to their bulk values.
• the driving force may be saline concentration gradient of the fluid stream.
• the saline concentration gradient of the fluid stream may be about 3 to about 1000, about 10 to about 1000, about 100 to about 1000, about 200 to about 1000, about 500 to about 1000, about 3 to about 10, about 3 to about 100, about 3 to about 200, about 3 to about 500, about 10 to about 100, about 10 to about 200, about 10 to about 500, about 100 to about 200, about 100 to about 500, or about 200 to about 500.
• the fluid stream may have an average saline concentration of about 2 mM to about 1.5 M, about 10 iTiM to about 1.5 M, about 100 mM to about 1.5 M, about 500 mM to about 1.5 M, about 1 M to about 1.5 M, about 2 mM to about 10 mM, about 2 mM to about 100 mM, about 2 mM to about 500 mM, about 2 mM to about 1 M, about 10 mM to about 100 mM, about 10 mM to about 500 mM, about 10 mM to about 1 M, about 100 mM to about 500 mM, about 100 mM to about 1 M, or about 500 mM to about 1 M, where the average concentration is the average value of the saline concentrations across both surfaces of the membrane.
• the device comprises a multi-layered membrane comprising a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; wherein the bottom layer comprises a hole with an area in the range of about 1 pm 2 to 1 mm 2 ; and wherein the hole is capable of being in fluid communication with the at least one channel of the spacer layer.
• the size of the hole may alternatively be in the range of about 10 pm 2 to about 1 mm 2 , about 100 pm 2 to about 1 mm 2 , about 1000 pm 2 to about 1 mm 2 , about 0.01 mm 2 to about 1 mm 2 , about 0.1 mm 2 to about 1 mm 2 , about 1 pm 2 to about 10 pm 2 , about 1 pm 2 to about 100 pm 2 , about 1 pm 2 to about 1000pm 2 , about 1 pm 2 to about 0.01 mm 2 , about 1 pm 2 to about 0.1 mm 2 , about 10 pm 2 to about 100 pm 2 , about 10 pm 2 to about 1000pm 2 , about 10 pm 2 to about 0.01 mm 2 , about 10 pm 2 to about 0.1 mm 2 , about 100 pm 2 to about 1000pm 2 , about 100 pm 2 to about 0.01 mm 2 , about 100 pm 2 to about 0.1 mm 2 , about 1000 pm 2 to about 0.01 mm 2 , about 1000 pm 2 to about 0.1 mm 2 , or about 0.01 mm 2
• the multi-layered membrane may be oriented parallel to the liquid interface between two liquids.
• the device may be altered such the device comprises a plurality of multi-layered membranes.
• the device may further comprise two or more chambers, wherein the multi-layered membrane may be placed between two chambers.
• Each of the chambers may be intended for receiving an electrolyte solution having a chemical potential.
• the device may further comprise electrodes partially or fully submerged in the electrolytic solution.
• each chamber containing the electrolyte solution is in direct contact with one electrode.
• a pair of electrodes may be configured such that the electrodes are connected via a generator load or electric load.
• the top layer of the multi-layered membrane may be in contact with only one chamber, while the bottom layer may be mostly in contact with another chamber.
• ions or molecules in the electrolytic solution may pass through the multi-layered membrane.
• Ionic species having different charge or valence may pass through the multi-layered membrane.
• the ionic species having different charge or valence may have enhanced mobility within the at least one channel of the multi-layered membrane and may diffuse through the at least one channel at different speed, resulting in the imbalance of the charge neutrality of the system, thus generating an osmotic voltage and/or osmotic current.
• the osmotic voltage and/or osmotic current may generate electrical energy, which may be collected by a generator load.
• the electrochemical potential may arise due to a saline concentration gradient between the various electrolyte solutions in the two or more chambers.
• the saline concentration gradient of about 3 to about 1000, about 10 to about 1000, about 100 to about 1000, about 200 to about 1000, about 500 to about 1000, about 3 to about 10, about 3 to about 100, about 3 to about 200, about 3 to about 500, about 10 to about 100, about 10 to about 200, about 10 to about 500, about 100 to about 200, about 100 to about 500, or about 200 to about 500, may generate an osmotic voltage and/or osmotic current in the device.
• the fluid within the two or more chambers may have an average saline concentration of about 2 mM to about 1.5 M, about 10 mM to about 1.5 M, about 100 mM to about 1.5 M, about 500 mM to about 1.5 M, about 1 M to about 1.5 M, about 2 mM to about 10 mM, about 2 mM to about 100 mM, about 2 mM to about 500 mM, about 2 mM to about 1 M, about 10 mM to about 100 mM, about 10 mM to about 500 mM, about 10 mM to about 1 M, about 100 mM to about 500 mM, about 100 mM to about 1 M, or about 500 mM to about 1 M, to generate an osmotic voltage and/or osmotic current in the device, where the average concentration is the average value of the saline concentrations in the two or more chambers of the device.
• the method or the device as disclosed herein can be used in osmotic power generation. There is thus provided use of the method as disclosed herein or the device as disclosed herein for osmotic power generation.
• a device comprising a multi-layered membrane for osmotic power generation wherein the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; and wherein the bottom layer comprises a hole that is capable of being in fluid communication with the at least one channel of the spacer layer.
• the hole in the bottom layer may have an area in the range of about 1 pm 2 to 1 mm 2 . Therefore, there is also provided use of a device comprising a multi-layered membrane for osmotic power generation wherein the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; and wherein the bottom layer comprises a hole with an area in the range of 1 pm 2 to 1 mm 2 ; and wherein the hole is capable of being in fluid communication with the at least one channel of the spacer layer.
• a method for generating osmotic power by separating a plurality of ions or molecules in a fluid stream comprising the steps of: a) providing a multi-layered membrane; b) contacting a first surface of the multi-layered membrane with the fluid stream under a driving force to selectively allow desired ions or molecules to pass through to a second surface; wherein first surface of the multi-layered membrane is optionally charged; and wherein the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; and wherein the bottom layer comprises a hole that is capable of being in fluid communication with the at least one channel of the spacer layer.
• the hole in the bottom layer may have an area in the range of about 1 pm 2 to 1 mm 2 . Therefore, there is also provided a method for generating osmotic power by separating a plurality of ions or molecules in a fluid stream comprising the steps of: a) providing a multi-layered membrane; b) contacting a first surface of the multi-layered membrane with the fluid stream under a driving force to selectively allow desired ions or molecules to pass through to a second surface; wherein first surface of the multi-layered membrane is optionally charged; and wherein the multi-layered membrane comprises a top layer, a bottom layer, and a spacer layer; wherein the spacer layer is interposed between the top layer and the bottom layer; wherein the top layer, the bottom layer and the spacer layer are each independently composed of one or more selective layers, each selective layer comprising a 2D material; wherein the spacer layer comprises at least one channel for receiving a fluid; wherein the bottom layer comprises a hole with an area in the range of 1
• each ion species or molecule may move at different mobilities as compared to each other, or when compared to the typical mobility when in a bulk phase. Due to the different mobilities between cations and anions, an osmotic voltage and osmotic current is generated, leading to a generation of osmotic power.
• the osmotic power generated (P) may be in the range of about 3 W/m 2 to about 10 kW/m 2 , of about 10 W/m 2 to about 10 kW/m 2 , about 100 W/m 2 to about 10 kW/m 2 , about 1 kW/m 2 to about 10 kW/m 2 , about 5 kW/m 2 to about 10 kW/m 2 , of about 3 W/m 2 to about 10 W/m 2 , about 3 W/m 2 to about 100 W/m 2 , about 3 W/m 2 to about 1 kW/m 2 , about 3 W/m 2 to about 5 kW/m 2 , about 10 W/m 2 to about 100 W/m 2 , about 10 W/m 2 to about 1 kW/m 2 , about 10 W/m 2 to about 5 kW/m 2 , about 100 W/m 2 to about 1 kW/m 2 , about 100 W/m 2 to about 5 kW/m 2 , or about 1 kW/m 2 to about 5
• the energy efficiency of osmotic power generation may be in the range of about 5 % to about 25 %, about 10 % to about 25 %, about 15 % to about 25 %, about 20 % to about 25 %, about 5 % to about 10 %, about 5 % to about 15 %, about 5 % to about 20 %, about 10 % to about 15 %, about 10 % to about 20 %, or about 15 % to about 20 %.
• FIG. 1 is a schematic illustration of the structure of a device comprising a multi-layered membrane (600) comprising a top layer, a bottom layer, and a spacer layer, wherein each chamber (400, 500) is intended for receiving an electrolyte solution with a given chemical potential, wherein each electrolyte solution is in direct contact with one electrode (200, 300), and the electrodes are configured to be connected to a generator load (100).
• the arrows show the movement of the ions due to diffusion from the higher saline concentration chamber (400) to the lower saline concentration chamber (500).
• FIG. 2A is an illustration of the structure of a multi-layered membrane (600) used in the device of Fig. 1.
• the multi-layered membrane (600) comprises of a bottom layer (700), a spacer layer (800) and a top layer (900), where the spacer layer (800) comprises an array of stacks of selective layers, such that each stack of selective layers (1000) is separated from the next by a channel (1100).
• the top layer (900) comprises of a top graphitic layer (2000) and a metal or metal oxide layer (2100). The directions of the arrows show the movement of the ions in the solution through the hole in the bottom layer and passing out from the channels (1100) of the spacer layer (800) .
• FIG. 2B is an illustration of the cross sectional view of the bottom layer (700) of the multi-layered membrane (600) used in the device of Fig. 1, which comprises of a bottom graphitic layer (1600) supported by a silicon nitride substrate layer (1200) and a silicon layer (1900).
• FIG. 2C is an illustration of the SiNx substrate layer (1200) used as the support for the bottom layer (700), where the 300 nm thick SiNx substrate (1200) has a rectangular hole (1300) of about 10 pm 2 in size, where length (1400) is about 10 pm and width (1500) is about 1 pm.
• Fig. 2D is an illustration of the SiNx substrate layer (1200) used as the support for the bottom layer (700), where the 300 nm thick SiNx substrate (1200) has a rectangular hole (1300) of about 10 pm 2 in size, where length (1400) is about 10 pm and width (1500) is about 1 pm.
• Fig. 2D is an illustration of the SiNx substrate layer (1200) used as the support for the bottom layer (700), where the 300 nm thick SiNx substrate (1200) has a rectangular hole (1300) of about 10 pm 2 in size, where length (1400) is about 10 pm and width (1500) is about 1 pm.
• Fig. 2D is an illustration of the SiNx substrate layer
• FIG. 2D is an illustration of the cross-sectional view of the spacer layer (800) of the multi-layered membrane (600) used in the device of Fig. 1 , comprising of stacks of selective layers, where each stack of selective layers (1000) has a height (1700) and is separated from the next stack of selective layers by a channel (1100) of a distance (1800).
• the distance (1800) is referred to as the width of the channel.
• the height of a channel is also represented by 1700, similar to the height of a stack of selective layers (1000).
• FIG. 3C is a plot showing the relationship between the transference number of the cation (K + ) of the device at different electrolyte concentrations but fixed diffusion potential (i.e. fixed concentration gradient of 3: 1), at heights of 7 A and 30 A of a channel (1100) of Fig. 2D.
• C av being the average value of the saline concentration in each of the chambers (400 and 500) of Fig. 1 (i.e. (C o +CD/2).
• FIG. 4A is a plot showing the ionic mobility of the device for the cations (K + ) and anions (Cl ) normalized to the ionic mobility of the solution (p/p Buik ) as a function of concentration gradient, while the inset plot show the ratio of the ionic mobility of the cations ((K + ) to anions (Cl ) as a function of concentration gradient.
• Ci and Co represents the saline concentration in each of the chambers (500 and 400) of Fig. 1.
• FIG. 4B is a plot showing the ionic mobility of the device for the cations (K + or Na + ) and anions (Cl ) normalized to the ionic mobility of the solution (m/m Bulk ) as a function of different electrolyte concentrations and different concentration gradient.
• Ci and Co represents the saline concentration in each of the chambers (400 and 500) of Fig. 1
• C avg represents the average value of the saline concentration in each of the chambers (400 and 500) of Fig. 1 (i.e. (C 0 +Ci)/2).
• FIG. 5A is a plot showing the maximum osmotic power generated (kW/m 2 ) in the device as a function of different salinity gradient and concentration when the height (1700, in angstrom, A) of a channel (1100) of Fig. 2D), is 7 A.
• FIG. 5B is a plot showing the maximum energy efficiency (%) in the device as a function of different salinity gradient and concentration when the height (1700, in angstrom, A) of a channel (1100) of Fig. 2D, is 7 A.
• FIG. 5C is a plot showing the relationship between the transference number of the cation (K + ) of the device at different electrolyte concentrations where the height (1700, in angstrom, A) of a channel (1100) of Fig. 2D, is at 7 A and 30 A, and the concentration gradient of varies from 3: 1 to 1000: 1.
• FIG. 5D is a plot showing the maximum osmotic power generated (kW/m 2 ) in the device as a function of the height (1700, in angstrom, A) of a channel (1100) of Fig. 2D, at a fixed concentration gradient of 100.
• SiNx silicon nitride
• the multi-layered membrane comprises a plurality of multi-layered structures stacked upon one another, wherein the spacer layer comprises an array of stacks of selective layers such that each stack of selective layer (1000) is separated from the next by a channel (1100).
• the multi-layered membrane has channels for passing the ions and molecules through the multi-layered membrane. Because of the difference in chemical potential of the electrolyte solutions between the two chambers (400, 500) of the device in Fig.
• ions or molecules will pass through the active multi-layered membrane (600). Ionic species with different charge or valence will have an enhanced mobility within the channels of the active multi-layered membrane and will diffuse through the channels at different speeds. This will cause an imbalance in the charge neutrality of the system, resulting in an osmotic current and osmotic potential. These osmotic potential and current generate an electrical power that is collected by the generator load (100) through the electrodes (200, 300).
• a prototype multi-layered membrane of trilayer structure as shown in Fig. 2A, three graphitic crystal layers were isolated by mechanical exfoliation.
• a thick graphite crystal is laid on a low-residue tape.
• the thick graphite crystal is then pressed between another piece of the same tape to cleave the graphite crystal into two pieces. The process is repeated for several times till the piece of tape is fully covered with such crystals.
• the final thickness of those flakes is between 0.3 nm to 500 pm, with an area size of few microns square to millimetre square.
• a graphitic crystal layer (1600) prepared by mechanical exfoliation as described above was transferred onto a substrate (1200) as shown in Fig. 2B, where the substrate (1200) is a 300 nm thick silicon nitride (SiNx) substrate (1200) with a rectangular hole (1300) of about 1 x 10 pm 2 as shown in Fig. 2C.
• This layer of SiNx substrate is supported by a layer of silicon (Si) substrate (1900).
• This graphitic layer (1600) is then etched by reactive ion etching using the rectangular hole (1300) in the SiNx substrate (1200) as an etch mask.
• the dimension of the hole in the graphitic layer (1600) is identical to that in the substrate (1200). Reference to the “hole” in the context of this disclosure is thus the hole that is present in the graphitic layer (1600).
• graphitic layers as selective layers each with a height ranging from 0.7 nm to 35 nm were exfoliated onto a 300 nm thick S1O2 substrate to form a stack of selective layers. Approximately 2 to 117 graphene layers as selective layers was used. The height (1700) of each stack of selective layers was confirmed by measuring using atomic force microscopy (Dimension FastScan, Bruker, USA) in tapping mode.
• This stack of selective layers is then patterned by electron beam lithography and dry etching onto the bottom graphitic layer, in an array of ribbons which are now stacks of selective layers, where each stack of selective layers (1000) is of several microns in width, 150 nm in length and spaced at a distance (1800) of 100 nm from each other, to form the second (spacer) graphitic layer as shown in Fig. 2D prior to stacking on top of the bottom layer.
• This spacer graphitic layer contains nanometer sized channels (1100) wherein the height (1700) of each channel (1100) is equivalent to the height of a stack of selective layers (1000) in the spacer layer.
• the selective layers in the spacer graphitic layer were annealed at 400 °C prior to assembling with the bottom layer. At this annealing temperature, contaminants such as hydrocarbons and polymer residues are removed.
• the stacks of selective layers are then released from the S1O2 substrate by a wet etching process and transferred with a polymeric film on top of the bottom layer (700) by a custom-made micromanipulator.
• the polymeric film was then removed from the stacks of selective layers by dipping the sample in acetone and isopropyl alcohol, followed by another step of annealing at 400 °C.
• a thick graphitic layer (2000) of about 50 to 120 nm was exfoliated on S1O2 and transferred in a manner like previously done for the spacer layer, on top of the spacer layer of the bottom layer/spacer layer assembly as a top graphitic layer, and a gold mask (2100) was deposited on top of the top graphitic layer (2000).
• a final dry etching step removes the part of the channels that is not protected by the gold layer (2100), hence defining the final length of the channels.
• the final dry etching step results in the extremes of the spacer layer (800) being flushed with the top layer (900), which may result in a better fit of the multi-layer membrane (600) to a device.
• the multi-layered membrane as synthesized in Example 1 was incorporated into a device as shown in Fig. 1 and subjected to testing to characterize the multi-layered membrane’s performance.
• the multi-layered membrane (600) was integrated perpendicular to the ionic solutions in the two chambers (400 and 500).
• Characterization of the ionic conductance of the multi-layered membrane was done using the Axopatch 200B Patch-Clamp Amplifier (Molecular Devices, USA). A voltage, sweeping at 200mV to 200mV, was applied between the two Ag/AgCl electrodes. The resulting current was measured by the Axonpatch 200B Patch-Clamp Amplifier. The multi-layered membrane conductance at each ionic concentration was then extracted from the slope of the measured current vs voltage curve. By using the Flenderson and GF1K formalism, the individual ionic mobilities were extracted.
• an enhanced ionic conductance (i.e. G/G Buik > 1) was observed in the device when the height of each channel in the spacer layer is at 3 nm or less, and this phenomenon was observed in the absence of a concentration gradient.
• This enhancement of ionic conductance may be due to different ionic mobilities of ions and molecules inside the channels as shown in Fig. 3B as compared to their bulk values, and their 2D physical confinement with these channels.
• ion -ion correlations become significant and the enhanced selectivity is disrupted.
• the ionic conductance is comparable to the bulk solution, indicating a complete disruption of the physical confinement effect and a smaller contribution of the surface conductivity to the total ionic conductance.
• Fig. 3B Based on the results of Fig. 3B , it was found that the ionic mobility of the ions inside the channels are higher than in a bulk solution, although it was expected that the ions inside a confined and restricted space would move equally or slower than in a bulk solution where they are free to move in any direction. Further, the results of Fig. 3B showed that the cations can move faster than the anions when the height of the channel is below 30 A, and hence the membrane is exhibiting cation selectivity. This is surprising because the cations K + have a similar size to the anions Cl- and it would be expected for the ionic mobilities of the two types of ions to be similar, however the results showed ionic selectivity, which in this case is for the cations K + .
• cationic transference number was extrapolated from the osmotic potential at different electrolyte concentrations with fixed diffusion potential (where concentration gradient was fixed at 3:1) as depicted in Fig. 3C.
• concentration gradient was fixed at 3:1
• Fig. 3C Based on the results of Fig. 3C, in the case of highly confined channels of height 7 A, the enhanced mobility of cations corresponds to a high anionic rejection. This surface -related effect becomes insignificant only at very high saline concentrations (for example more than 1 M) when ion-ion correlations become significant. In less confined systems as seen for channels of height 30 A, cation selectivity was not observed.
• anions Cl ions show a higher diffusivity than cations K + because of the chemical interaction of K + ions with the graphitic surface of the multi-layered membrane.
• the effect of higher anion diffusivity is progressively reduced until it is completely cancelled for concentrations above 0.1 M.
• Fig. 4A represents the ionic mobility of K + cations and Cl anions normalized with respect to their bulk values under a saline concentration gradient
• K + cations move faster with respect to the Cl anions as show in the inset diagram.
• Fig. 4A showed that when saline concentration gradients equal or bigger than 3 both Cl and K + ions show enhanced ionic mobility with respect to the bulk solution.
• Fig. 4B which represents the ionic mobility of cations and anions normalized with respect to their bulk values under a saline concentration gradient of 3 or 10.
• a saline concentration gradient of 3 or 10.
• anions show minimal variation of ionic mobility with respect to the bulk while cations show an increased mobility for each saline concentration gradient.
• This cation ionic mobility enhancement (valid both for K + and Na + ) is inversely proportional to the average saline concentration inside the channels of the multi-layered membrane.
• the maximum osmotic power generated (Fig. 5A), maximum energy efficiency (Fig. 5B) and cationic transference number (Fig. 5C) were obtained.
• the membrane and multi-layered membrane as disclosed herein may be deposited on a support or embedded in a matrix, to serve as an active membrane when it is incorporated into another membrane or system.
• the method as disclosed herein comprises the use of a membrane or multi-layered membrane which has ionic selectivity, an osmotic voltage and / or an osmotic current may be generated and thus, the method may be suitable for blue energy generation and storage where there is salinity gradient, for example in water desalination plants, nanofiltration, ion-exchange, brine -disposal and water filtration operations, and may find many commercial applications in water purification, pharmaceutical, chemical and fuel separation industries.
• the device as disclosed herein may be energy efficient and generate high power densities suitable for commercial blue energy recovery applications.

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